US20170253791A1 - Improved performance of crosslinked fracturing fluids comprising a nonionic surfactant - Google Patents
Improved performance of crosslinked fracturing fluids comprising a nonionic surfactant Download PDFInfo
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- US20170253791A1 US20170253791A1 US15/517,411 US201515517411A US2017253791A1 US 20170253791 A1 US20170253791 A1 US 20170253791A1 US 201515517411 A US201515517411 A US 201515517411A US 2017253791 A1 US2017253791 A1 US 2017253791A1
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- 239000012530 fluid Substances 0.000 title claims abstract description 42
- 239000002736 nonionic surfactant Substances 0.000 title claims abstract description 16
- 239000000203 mixture Substances 0.000 claims abstract description 55
- 229920000642 polymer Polymers 0.000 claims abstract description 18
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 16
- 239000003431 cross linking reagent Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000004094 surface-active agent Substances 0.000 claims description 33
- 239000012267 brine Substances 0.000 claims description 13
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 13
- 239000000243 solution Substances 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 9
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 5
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims description 4
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 claims description 4
- 229910052723 transition metal Inorganic materials 0.000 claims description 4
- 150000003624 transition metals Chemical class 0.000 claims description 4
- 238000004132 cross linking Methods 0.000 claims description 3
- 238000005755 formation reaction Methods 0.000 abstract description 11
- 239000004971 Cross linker Substances 0.000 description 8
- 229920002257 Plurafac® Polymers 0.000 description 6
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 6
- 229910052726 zirconium Inorganic materials 0.000 description 6
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical class [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 5
- 239000003381 stabilizer Substances 0.000 description 5
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Chemical compound [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 description 4
- 239000008399 tap water Substances 0.000 description 4
- 235000020679 tap water Nutrition 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000007046 ethoxylation reaction Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 244000007835 Cyamopsis tetragonoloba Species 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 229920002222 Plurafac® RA 300 Polymers 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 239000003139 biocide Substances 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229920001477 hydrophilic polymer Polymers 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002455 scale inhibitor Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 230000000638 stimulation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/62—Compositions for forming crevices or fractures
- C09K8/66—Compositions based on water or polar solvents
- C09K8/68—Compositions based on water or polar solvents containing organic compounds
- C09K8/685—Compositions based on water or polar solvents containing organic compounds containing cross-linking agents
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
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- A61K31/21—Esters, e.g. nitroglycerine, selenocyanates
- A61K31/215—Esters, e.g. nitroglycerine, selenocyanates of carboxylic acids
- A61K31/22—Esters, e.g. nitroglycerine, selenocyanates of carboxylic acids of acyclic acids, e.g. pravastatin
- A61K31/225—Polycarboxylic acids
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- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/33—Heterocyclic compounds
- A61K31/395—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
- A61K31/435—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with one nitrogen as the only ring hetero atom
- A61K31/47—Quinolines; Isoquinolines
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- A61K45/06—Mixtures of active ingredients without chemical characterisation, e.g. antiphlogistics and cardiaca
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/34—Esters of acyclic saturated polycarboxylic acids having an esterified carboxyl group bound to an acyclic carbon atom
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D215/00—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems
- C07D215/02—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom
- C07D215/16—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D215/48—Carbon atoms having three bonds to hetero atoms with at the most one bond to halogen
- C07D215/54—Carbon atoms having three bonds to hetero atoms with at the most one bond to halogen attached in position 3
- C07D215/56—Carbon atoms having three bonds to hetero atoms with at the most one bond to halogen attached in position 3 with oxygen atoms in position 4
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/602—Compositions for stimulating production by acting on the underground formation containing surfactants
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/62—Compositions for forming crevices or fractures
- C09K8/66—Compositions based on water or polar solvents
- C09K8/665—Compositions based on water or polar solvents containing inorganic compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/62—Compositions for forming crevices or fractures
- C09K8/66—Compositions based on water or polar solvents
- C09K8/68—Compositions based on water or polar solvents containing organic compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/84—Compositions based on water or polar solvents
- C09K8/845—Compositions based on water or polar solvents containing inorganic compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/84—Compositions based on water or polar solvents
- C09K8/86—Compositions based on water or polar solvents containing organic compounds
- C09K8/88—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/84—Compositions based on water or polar solvents
- C09K8/86—Compositions based on water or polar solvents containing organic compounds
- C09K8/88—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
- C09K8/887—Compositions based on water or polar solvents containing organic compounds macromolecular compounds containing cross-linking agents
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B37/00—Methods or apparatus for cleaning boreholes or wells
- E21B37/06—Methods or apparatus for cleaning boreholes or wells using chemical means for preventing or limiting, e.g. eliminating, the deposition of paraffins or like substances
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B41/00—Equipment or details not covered by groups E21B15/00 - E21B40/00
- E21B41/02—Equipment or details not covered by groups E21B15/00 - E21B40/00 in situ inhibition of corrosion in boreholes or wells
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
- E21B43/267—Methods for stimulating production by forming crevices or fractures reinforcing fractures by propping
Definitions
- the presently disclosed subject matter relates to a gel composition containing a nonionic surfactant and use of the gel composition in oilfield applications.
- a gel composition for use in a subterranean formation can include a base fluid, a cross-linkable polymer soluble in the base fluid, a cross-linking agent and a nonionic surfactant.
- the base fluid can be a brine solution.
- FIG. 1 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 12% KCl salt, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments.
- FIG. 2 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 6% KCl salt, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments.
- FIG. 3 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 2% KCl salt, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments.
- FIG. 4 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., 9 ppg brine, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments.
- FIG. 5 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 9 ppg mixed brine, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments.
- FIG. 6 is a graph showing viscosity vs. time for 3.6 grams/liter CMHPG at 240 degrees F., filtered produced water with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments.
- the gel composition can comprise a base fluid, a cross-linkable polymer that is soluble in the base fluid, a nonionic surfactant and a cross-linking agent.
- the gel composition has improved crosslinked stability.
- the gel composition can be injected into the subterranean formation as a fracturing fluid and allowed to penetrate the formation.
- the fracturing fluid can transport a proppant into the fracture to keep the frature open to produce oil and gas.
- the gel composition provides improved performance for crosslinked fracturing fluids in produced waters.
- the base fluid can be a brine solution.
- the brine solution can comprise, for example, a solution of salt (such as sodium chloride) in water.
- materials that can be present in the brine solution can include mono and divalent salts that include potassium chloride, sodium bromide, a sodium bromide/calcium chloride mixture, or a produced brine such as produced water.
- the brine solution can be any solution that contains salts.
- the nonionic surfactant has been shown to improve the stability of the crosslinked fluids at temperatures greater than 200° F. when mixed with base fluids composed of the above described brines.
- the cross-linkable polymer can be a hydrophilic polymer that is generally soluble in the base fluid and is capable of being cross-linked in solution so that the polymer interconnects to form a semi-solid gel.
- these polymers are well known to those skilled in the art.
- cross-linkable polymers that can be utilized according to the presently disclosed subject matter can include, for example, guar gum and guar derivatives.
- Other suitable cross-linkable polymers may also be used in forming the gel composition of the presently disclosed subject matter, and are well known and will be readily apparent to those skilled in the art.
- cross-linking agents are also well known to those skilled in the art.
- suitable cross-linking agents can include, for example transition metal crosslinkers. These cross-linking agents bond ionically with the polymers to form the cross-linked molecule.
- Other suitable cross-linking agents may be used in forming the gel composition of the presently disclosed subject matter, and are well known and will be readily apparent to those skilled in the art.
- the amount of cross-linking agent that is used will typically vary depending upon the type of polymer and the degree of cross-linking desired.
- the gel composition of the presently disclosed subject matter can further comprise a nonionic surfactant.
- nonionic surfactants that may be used according to the presently disclosed subject matter include Plurafac® versions SLF 45, SLF 18B45, SLF 180, RA 300, LF 400 and/or LF 900, and Dehypon LS 36 which are commercially available from BASF Corporation of Mount Olive, N.J., and Antarox® version BL 759, which is commercially available from Novecare Solvay.
- EO/PO non-ionic alcohol ethylene oxide/propylene oxide
- the nonionic surfactant should be present in the gel composition in an amount sufficient to provide the desired properties.
- the nonionic surfactant is present in the gel composition of the presently disclosed subject matter in an amount in the range from about 0.0170% to about 0.1013% by weight.
- a non-ionic alcohol surfactant can be utilized having a hydrocarbon chain in the range from C 10 to C 16 and in the range from 5-80 moles of EO (ethoxylation) and in the range from 3-60 moles of PO (propoxylation).
- the EO/PO ratio of the surfactant can be in the range from 1:2 to 4:2.
- the hydrophilic-lipophilic balance (or “HLB”) of the surfactant can be in the range from 11 to 14 and the surfactant is water soluble.
- the gel composition of the presently disclosed subject matter can be a metallic crosslinked fracturing fluid.
- the metallic component of the gel composition can be a transition metal.
- nonionic surfactant such as those described above inhibits the interaction between the metal cations of the brine and the cross-linkable polymer that normally cause the transition metal crosslinked fluids to lose stability.
- additives suitable for use in operations in subterranean formations also may be added to the gel composition.
- These other additives can include, but are not limited to, proppants, biocide, scale inhibitor, corrosion inhibitor, paraffin inhibitor, asphaletene inhibitor, iron control and other commonly used oilfield chemicals and combinations thereof.
- proppants biocide, scale inhibitor, corrosion inhibitor, paraffin inhibitor, asphaletene inhibitor, iron control and other commonly used oilfield chemicals and combinations thereof.
- a gel composition comprising a base fluid, a cross-linkable polymer that is soluble in the base fluid, and a cross-linking agent.
- a nonionic surfactant can be added to the gel composition.
- the nonionic surfactant can include Plurafac® versions SLF 45, SLF 18B45, SLF 180, RA 300, LF 400 and/or LF 900, and Dehypon LS 36 which are commercially available from BASF Corporation of Mount Olive, N.J., and Antarox® version BL 759, which is commercially available from Novecare Solvay.
- the gel composition can include a non-ionic alcohol surfactant having a hydrocarbon chain in the range from C 10 to C 16 and in the range from 5-80 moles of EO (ethoxylation) and in the range from 3-60 moles of PO (propoxylation).
- the EO/PO ratio of the surfactant can be in the range from 1:2 to 4:2.
- the hydrophilic-lipophilic balance (or “HLB”) of the surfactant can be in the range from 11 to 14 and the surfactant is water soluble.
- the gel composition can be injected into the opening in the subterranean formation and cross-linked to increase the size of the opening.
- the cross linked gel composition can cause more width to occur in the opening. It is believed that the nonionic surfactant does not interfere with the cross-linking process and can provide adequate properties without adversely affecting the ability of the gel composition to be injected into the opening.
- the gel composition described herein provides a stable crosslinked fluid for use as a high density completions fluid for offshore stimulations.
- the gel composition described herein can be stable at high temperatures, such as 275° F. or above, with produced waters with high total dissolved solids (“TDS”) without the need for dilution or expensive water treatments.
- the polymer was added to the brine solution and allowed to hydrate for 30 minutes, using a standard Servodyne mixer with a high efficiency paddle at approximately 1000 rpm. Once the fluid was completely hydrated the fluid was buffered to the appropriate pH, crosslinker added, and then loaded into a Chandler 5550 cup.
- the fluid was initially run through a shear rate sweep of 100, 75, 50, and 25 sec ⁇ 1 to calculate the power law indices n′ and K′ at ambient temperature. After this initial sweep the set temperature ramp initiates and begins to heat up the fluid. The fluid was then sheared at 100 sec ⁇ 1 for 20 minutes. After 20 minutes of constant shear 100 sec ⁇ 1 , the fluid runs through another shear rate sweep this time at temperature. Again fluid is sheared at 100 sec ⁇ 1 in between shear rate sweeps and the shear rate sweep repeated every 15 minutes for 2 hours 5 minute then every 30 minutes for the next hour. A RIBS rotor-bob configuration was used.
- Example 1 The results of the testing from Example 1 are shown in FIGS. 1-6 hereto, where Surfactant A is Anatrox BL 759, Surfactant B is Plurafac SFL 45, Surfactant C is Plurafac SFL 180, Surfactant D is Plurafac RA 300, Surfactant E is Plurafac LF 400 and Surfactant F is Plurafac LF 900. Shear rate sweep data was removed from all figures for better analysis of the fluid's viscosity. There is improved viscosity performance when utilizing the subject surfactants relative to the baselines for all the figures. Example 1 demonstrates that with the addition of the surfactant, the fluid has more viscosity for a longer period of time.
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Abstract
Description
- This patent application claims the benefit, and priority benefit, of U.S. Provisional Patent Application Ser. No. 62/060,826, filed Oct. 7, 2014, the contents of which are incorporated by reference herein in its entirety.
- The presently disclosed subject matter relates to a gel composition containing a nonionic surfactant and use of the gel composition in oilfield applications.
- According to the illustrative embodiments disclosed herein, a gel composition for use in a subterranean formation is provided. The gel composition can include a base fluid, a cross-linkable polymer soluble in the base fluid, a cross-linking agent and a nonionic surfactant. In certain illustrative embodiments, the base fluid can be a brine solution.
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FIG. 1 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 12% KCl salt, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments. -
FIG. 2 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 6% KCl salt, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments. -
FIG. 3 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 2% KCl salt, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments. -
FIG. 4 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., 9 ppg brine, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments. -
FIG. 5 is a graph showing viscosity vs. time for 4.8 grams/liter CMHPG at 250 degrees F., tap water with 9 ppg mixed brine, a gel stabilizer with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments. -
FIG. 6 is a graph showing viscosity vs. time for 3.6 grams/liter CMHPG at 240 degrees F., filtered produced water with a pH of 6 and a zirconium crosslinker in certain illustrative embodiments. - While certain preferred illustrative embodiments will be described herein, it will be understood that this description is not intended to limit the subject matter to those embodiments. On the contrary, it is intended to cover all alternatives, modifications, and equivalents, as may be included within the spirit and scope of the subject matter as defined by the appended claims.
- Disclosed herein is a gel composition for use in subterranean formations. In certain illustrative embodiments, the gel composition can comprise a base fluid, a cross-linkable polymer that is soluble in the base fluid, a nonionic surfactant and a cross-linking agent. In certain illustrative embodiments, the gel composition has improved crosslinked stability. The gel composition can be injected into the subterranean formation as a fracturing fluid and allowed to penetrate the formation. The fracturing fluid can transport a proppant into the fracture to keep the frature open to produce oil and gas. The gel composition provides improved performance for crosslinked fracturing fluids in produced waters.
- In certain illustrative embodiments, the base fluid can be a brine solution. The brine solution can comprise, for example, a solution of salt (such as sodium chloride) in water. Other examples of materials that can be present in the brine solution can include mono and divalent salts that include potassium chloride, sodium bromide, a sodium bromide/calcium chloride mixture, or a produced brine such as produced water. In general, the brine solution can be any solution that contains salts. In certain illustrative embodiments, the nonionic surfactant has been shown to improve the stability of the crosslinked fluids at temperatures greater than 200° F. when mixed with base fluids composed of the above described brines.
- In certain illustrative embodiments, the cross-linkable polymer can be a hydrophilic polymer that is generally soluble in the base fluid and is capable of being cross-linked in solution so that the polymer interconnects to form a semi-solid gel. Examples of these polymers are well known to those skilled in the art. Examples of cross-linkable polymers that can be utilized according to the presently disclosed subject matter can include, for example, guar gum and guar derivatives. Other suitable cross-linkable polymers may also be used in forming the gel composition of the presently disclosed subject matter, and are well known and will be readily apparent to those skilled in the art.
- Various cross-linking agents are also well known to those skilled in the art. Examples of suitable cross-linking agents according to the presently disclosed subject matter can include, for example transition metal crosslinkers. These cross-linking agents bond ionically with the polymers to form the cross-linked molecule. Other suitable cross-linking agents may be used in forming the gel composition of the presently disclosed subject matter, and are well known and will be readily apparent to those skilled in the art. The amount of cross-linking agent that is used will typically vary depending upon the type of polymer and the degree of cross-linking desired.
- The gel composition of the presently disclosed subject matter can further comprise a nonionic surfactant. Examples of nonionic surfactants that may be used according to the presently disclosed subject matter include Plurafac® versions SLF 45, SLF 18B45, SLF 180, RA 300, LF 400 and/or LF 900, and Dehypon LS 36 which are commercially available from BASF Corporation of Mount Olive, N.J., and Antarox® version BL 759, which is commercially available from Novecare Solvay. In certain illustrative embodiments, the use of non-ionic alcohol ethylene oxide/propylene oxide (“EO/PO”) surfactants such as those described above provides improved viscosity at temperature for the crosslinked fluids.
- The nonionic surfactant should be present in the gel composition in an amount sufficient to provide the desired properties. For example, in certain illustrative embodiments, the nonionic surfactant is present in the gel composition of the presently disclosed subject matter in an amount in the range from about 0.0170% to about 0.1013% by weight.
- In certain illustrative embodiments, a non-ionic alcohol surfactant can be utilized having a hydrocarbon chain in the range from C10 to C16 and in the range from 5-80 moles of EO (ethoxylation) and in the range from 3-60 moles of PO (propoxylation). Preferably, the EO/PO ratio of the surfactant can be in the range from 1:2 to 4:2. Further, in certain illustrative embodiments the hydrophilic-lipophilic balance (or “HLB”) of the surfactant can be in the range from 11 to 14 and the surfactant is water soluble.
- In certain illustrative embodiments, the gel composition of the presently disclosed subject matter can be a metallic crosslinked fracturing fluid. For example, the metallic component of the gel composition can be a transition metal.
- Without wishing to be bound by theory, it is believed that the nonionic surfactant such as those described above inhibits the interaction between the metal cations of the brine and the cross-linkable polymer that normally cause the transition metal crosslinked fluids to lose stability.
- Other additives suitable for use in operations in subterranean formations also may be added to the gel composition. These other additives can include, but are not limited to, proppants, biocide, scale inhibitor, corrosion inhibitor, paraffin inhibitor, asphaletene inhibitor, iron control and other commonly used oilfield chemicals and combinations thereof. A person having ordinary skill in the art, with the benefit of this disclosure, will know the type and amount of additive useful for a particular application and desired result.
- Various methods of treating subterranean formations using a gel composition containing a nonionic surfactant are also disclosed herein. For example, disclosed herein is a method of treating an opening in a subterranean formation. A gel composition is provided comprising a base fluid, a cross-linkable polymer that is soluble in the base fluid, and a cross-linking agent. A nonionic surfactant can be added to the gel composition. In certain illustrative embodiments, the nonionic surfactant can include Plurafac® versions SLF 45, SLF 18B45, SLF 180, RA 300, LF 400 and/or LF 900, and Dehypon LS 36 which are commercially available from BASF Corporation of Mount Olive, N.J., and Antarox® version BL 759, which is commercially available from Novecare Solvay. In certain illustrative embodiments, the gel composition can include a non-ionic alcohol surfactant having a hydrocarbon chain in the range from C10 to C16 and in the range from 5-80 moles of EO (ethoxylation) and in the range from 3-60 moles of PO (propoxylation). Preferably, the EO/PO ratio of the surfactant can be in the range from 1:2 to 4:2. Further, the hydrophilic-lipophilic balance (or “HLB”) of the surfactant can be in the range from 11 to 14 and the surfactant is water soluble. The gel composition can be injected into the opening in the subterranean formation and cross-linked to increase the size of the opening. For example, the cross linked gel composition can cause more width to occur in the opening. It is believed that the nonionic surfactant does not interfere with the cross-linking process and can provide adequate properties without adversely affecting the ability of the gel composition to be injected into the opening.
- In certain illustrative embodiments, the gel composition described herein provides a stable crosslinked fluid for use as a high density completions fluid for offshore stimulations. The gel composition described herein can be stable at high temperatures, such as 275° F. or above, with produced waters with high total dissolved solids (“TDS”) without the need for dilution or expensive water treatments.
- To facilitate a better understanding of the presently disclosed subject matter, the following examples of certain aspects of certain embodiments are given. In no way should the following examples be read to limit, or define, the scope of the presently disclosed subject matter.
- The polymer was added to the brine solution and allowed to hydrate for 30 minutes, using a standard Servodyne mixer with a high efficiency paddle at approximately 1000 rpm. Once the fluid was completely hydrated the fluid was buffered to the appropriate pH, crosslinker added, and then loaded into a Chandler 5550 cup. For API testing, the fluid was initially run through a shear rate sweep of 100, 75, 50, and 25 sec−1 to calculate the power law indices n′ and K′ at ambient temperature. After this initial sweep the set temperature ramp initiates and begins to heat up the fluid. The fluid was then sheared at 100 sec−1 for 20 minutes. After 20 minutes of
constant shear 100 sec−1, the fluid runs through another shear rate sweep this time at temperature. Again fluid is sheared at 100 sec−1 in between shear rate sweeps and the shear rate sweep repeated every 15 minutes for 2 hours 5 minute then every 30 minutes for the next hour. A RIBS rotor-bob configuration was used. - The results of the testing from Example 1 are shown in
FIGS. 1-6 hereto, where Surfactant A is Anatrox BL 759, Surfactant B is Plurafac SFL 45, Surfactant C is Plurafac SFL 180, Surfactant D isPlurafac RA 300, Surfactant E isPlurafac LF 400 and Surfactant F isPlurafac LF 900. Shear rate sweep data was removed from all figures for better analysis of the fluid's viscosity. There is improved viscosity performance when utilizing the subject surfactants relative to the baselines for all the figures. Example 1 demonstrates that with the addition of the surfactant, the fluid has more viscosity for a longer period of time. - It is to be understood that any recitation herein of numerical ranges by endpoints includes all numbers subsumed within the recited ranges as well as the endpoints of the range and equivalents.
- While the disclosed subject matter has been described in detail in connection with a number of embodiments, it is not limited to such disclosed embodiments. Rather, the disclosed subject matter can be modified to incorporate any number of variations, alterations, substitutions or equivalent arrangements not heretofore described, but which are commensurate with the scope of the disclosed subject matter. Additionally, while various embodiments of the disclosed subject matter have been described, it is to be understood that aspects of the disclosed subject matter may include only some of the described embodiments. Accordingly, the disclosed subject matter is not to be seen as limited by the foregoing description, but is only limited by the scope of the appended claims.
Claims (18)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US15/517,411 US20170253791A1 (en) | 2014-10-07 | 2015-10-07 | Improved performance of crosslinked fracturing fluids comprising a nonionic surfactant |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201462060826P | 2014-10-07 | 2014-10-07 | |
| PCT/US2015/054476 WO2016057659A1 (en) | 2014-10-07 | 2015-10-07 | Improved performance of crosslinked fracturing fluids comprising a nonionic surfactant |
| US15/517,411 US20170253791A1 (en) | 2014-10-07 | 2015-10-07 | Improved performance of crosslinked fracturing fluids comprising a nonionic surfactant |
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| US20170253791A1 true US20170253791A1 (en) | 2017-09-07 |
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| US15/517,411 Abandoned US20170253791A1 (en) | 2014-10-07 | 2015-10-07 | Improved performance of crosslinked fracturing fluids comprising a nonionic surfactant |
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| US (1) | US20170253791A1 (en) |
| MX (1) | MX2017004404A (en) |
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| WO (1) | WO2016057659A1 (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4995463A (en) * | 1990-06-04 | 1991-02-26 | Atlantic Richfield Company | Method for fracturing coal seams |
| US20070025683A1 (en) * | 2005-07-27 | 2007-02-01 | Seiko Epson Corporation | Moving image display device and moving image display method |
| US20090313772A1 (en) * | 2008-06-18 | 2009-12-24 | Charles Bullick Talley | Composition comprising peroxygen and surfactant compounds and method of using the same |
| US20100084134A1 (en) * | 2007-03-02 | 2010-04-08 | Trican Well Service Ltd. | Fracturing method and apparatus utilizing gelled isolation fluid |
| US20140274823A1 (en) * | 2013-03-15 | 2014-09-18 | U.S. O'neill Industries, Inc. | Hydrocarbon removal compositions and methods of use |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6820694B2 (en) * | 2002-04-23 | 2004-11-23 | Schlumberger Technology Corporation | Method for preparing improved high temperature fracturing fluids |
| US20070256836A1 (en) * | 2006-05-05 | 2007-11-08 | Halliburton Energy Services, Inc. | Methods of treating a subterranean formation with a treatment fluid having surfactant effective to increase the thermal stability of the fluid |
-
2015
- 2015-10-07 WO PCT/US2015/054476 patent/WO2016057659A1/en not_active Ceased
- 2015-10-07 MX MX2017004404A patent/MX2017004404A/en unknown
- 2015-10-07 RU RU2017113908A patent/RU2017113908A/en not_active Application Discontinuation
- 2015-10-07 US US15/517,411 patent/US20170253791A1/en not_active Abandoned
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4995463A (en) * | 1990-06-04 | 1991-02-26 | Atlantic Richfield Company | Method for fracturing coal seams |
| US20070025683A1 (en) * | 2005-07-27 | 2007-02-01 | Seiko Epson Corporation | Moving image display device and moving image display method |
| US20100084134A1 (en) * | 2007-03-02 | 2010-04-08 | Trican Well Service Ltd. | Fracturing method and apparatus utilizing gelled isolation fluid |
| US20090313772A1 (en) * | 2008-06-18 | 2009-12-24 | Charles Bullick Talley | Composition comprising peroxygen and surfactant compounds and method of using the same |
| US20140274823A1 (en) * | 2013-03-15 | 2014-09-18 | U.S. O'neill Industries, Inc. | Hydrocarbon removal compositions and methods of use |
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| RU2017113908A3 (en) | 2018-11-19 |
| RU2017113908A (en) | 2018-11-19 |
| MX2017004404A (en) | 2017-07-04 |
| WO2016057659A1 (en) | 2016-04-14 |
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